Polyamide monofilament suture manufactured from higher order polyamide

ABSTRACT

A higher order polyamide monofilament suture exhibits improved properties such as greater resistance to creep, greater knot security and greater chemical stability in aqueous environments.

This is a continuation of copending application Ser. No. 07/828,005 filed on Jan. 30, 1992, now abandoned.

BACKGROUND OF THE INVENTION

This invention relates to a polyamide (nylon) monofilament suture and, more particularly, to such a suture manufactured from a higher order polyamide such as nylon 12.

Polyamide monofilament sutures are known. Illustrative of the known processes for the melt spinning of polyamide strands (filament,yarn, etc.) are those described in U.S. Pat. Nos. 2,212,772; 2,226,549; 3,091,016; 3,303,169; 3,345,445; 3,361,859; 3,379,810; 3,382,307; 3,577,500; 4,009,511; 4,374,797; 4,446,299; 4,461,740; 4,504,432; 4,504,545; 4,542,063; 4,578,421; 4,621,021; 4,624,816; 4,701,377; 4,758,472; 4,839,132; and, 4,859,389.

One important characteristic of a suture is the amount of effort typically required to straighten the suture upon its removal from the package in order to ready the suture for use. In the case of a polyamide monofilament suture, this effort appears to be related to the "energy" of the suture, i.e., the integrations of the stress-strain curve for the suture measured in kilograms, and is equivalent to the work expended in elongating the monofilament by a specified percentage of its original length. As the energy of a given size of polyamide monofilament suture is less so, too, the amount of effort required to straighten the suture prior to use is less.

Another important consideration in the manufacture and use of sutures is that a yarn may stretch when under tension for an extended period of time. Under the tension of a surgeon's knot used for wound closure, a suture may undergo stretching which will cause the ligature to loosen, a phenomenon referred to herein as "creep".

Commonly owned copending U.S. patent application Ser. No. 07/828,010 filed Jan. 30, 1992 describes a process for manufacturing a polyamide monofilament suture from such nylons as nylon 6 and nylon 6,6 which exhibits reduced energy and/or an increased ability to retain a knot for a given suture when compared to prior polyamide sutures.

The present invention provides a suture exhibiting excellent dimensional stability, or resistance to creep, and high levels of strength retention and chemical stability when exposed to aqueous environments. The present invention further provides a suture exhibiting increased knot security or stability.

SUMMARY OF THE INVENTION

In accordance with the present invention, there is provided a polyamide monofilament suture manufactured from a higher order polyamide, i.e, a fiber-forming polyamide homopolymer or copolymer possessing a substantial number of repeating units selected from the group consisting of units of the structure ##STR1## in which n is at least about 7 and units of the structure ##STR2## in which R¹ is an aliphatic group of from about 4 to about 20 carbon atoms, a cycloaliphatic group of from about 6 to about 20 carbon atoms or an aromatic group of from about 6 to about 20 carbon atoms and R² is an aliphatic, cycloaliphatic or aromatic group of from about 6 to about 20 carbon atoms, provided, R¹ contains at least 6 carbon atoms when R² is an aliphatic group of 6 carbon atoms or R² contains at least 8 carbon atoms when R¹ contains 4 carbon atoms.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1A is a schematic illustration of apparatus which is suitable for manufacturing the high order polyamide monofilament suture of this invention; and,

FIG. 1B is a modification of the apparatus of FIG. 1A which is particularly suitable for the manufacture of polyamide monofilaments of smaller size, e.g., sizes 4/0 and smaller.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

The preferred higher order polyamides from which the suture of this invention can be manufactured contain at least about 30 mole percent, preferably at least about 50 mole percent and most preferably at least about 70 mole percent of units of the structure ##STR3## and/or the structure ##STR4## in which m, R¹ and R² have the above-designated meanings.

The higher order fiber-forming polyamides can be prepared by polymerizing aminocarboxylic acid and/or corresponding lactam or by polymerizing substantially equimolar proportions of diamine and dicarboxylic acid or functional derivative thereof such as an ester or acid chloride employing known and conventional techniques. Examples of the aforementioned aminocarboxylic acids or lactams thereof which are useful in preparing the higher order polyamides include those compounds containing at least about 8, preferably at least about 10 and most preferably at least about 12 carbon atoms. Particular examples of useful aminocarboxylic acids and lactams include capryllactam, 10-aminodecanoic acid, 11-aminoundecanoic acid and laurolactam, and the like.

Diamines suitable for use in preparation of the higher order fiber-forming polyamides include the straight chain and branched chain alkyl, aryl and alkaryl diamines. Such diamines include, e.g., those represented by the general formula

    H.sub.2 N(CH.sub.2).sub.m NH.sub.2

wherein m is an integer of at least about 6 and preferably at least about 12. Suitable diamines include hexamethylene diamine, octamethylene diamine, trimethylhexamethylene diamine, m-phenylene diamene and m-xylylene diamine.

The useful dicarboxylic acids can be represented by the formula

    HOOC--W--COOH

wherein W is a divalent aliphatic or aromatic group containing at least 6 carbon atoms. Suitable aliphatic acids include sebacic acid, suberic acid, azelaic acid, pimellic acid and adipic acid. Suitable aromatic acids include isophthalic acid and terephthalic acid.

Typical examples of the polyamide or nylon (as it is often called) resin used in the present invention are nylon 11, 12, 6/9, 6/12 and other higher order polyamides. Nylon 12 is an especially preferred fiber-forming polyamide resin from which the suture of this invention can be manufactured. In general, useful higher order polyamides will possess a number average molecular weight of at least about 10,000 and a melt flow index in g/10 min. of from about 1.5 to about 7.5.

Also included are block and random copolymers formed from one or more of the foregoing monomers and one or more other monomers copolymerizable therewith, e.g., lactones, alpha-hydroxy carboxylic acids and oligomers thereof, aminocarboxylic acids and/or corresponding lactams in addition to those mentioned, etc. Suitable lactones include gamma-butyrolactone and epsilon caprolactone. Suitable alpha-hydroxy carboxylic acids include hydroxybutanoic acid and hydroxycaproic acid. Useful higher order polyamides also include any of the foregoing homopolymers and copolymers blended with one or more compatible polymers, e.g., unlimited amounts of other polyamide homopolymers and/or polyamide copolymers, relatively minor amounts of polyester homopolymers and/or polyester copolymers, polyurethanes, etc.

A suitable process for the manufacture of the higher order polyamide monofilament suture of the present invention is disclosed and claimed in commonly assigned, concurrently filed U.S. patent application Ser. No. 07/828,010, filed Jan. 30, 1992, the contents of which are incorporated by reference herein. The process comprises the operations of extruding the polyamide resin at an extrusion temperature of from about 180° to about 290° C. to provide a monofilament, stretching the solidified monofilament at a temperature of from about 40° to about 98° C. in water (or other suitable liquid medium) or at from about 50° to about 185° C. in air (or other suitable gaseous medium) at a stretch ratio of from about 3:1 to about 5:1 to provide a stretched monofilament and annealing (relaxing) the stretched monofilament at a temperature of from about 100° to about 240° C. to provide the finished suture, the annealing resulting in shrinkage of the stretched monofilament for a recovery to within about 80% to about 97% of the length of the monofilament prior to annealing.

FIG. 1A schematically illustrates a higher order polyamide monofilament suture manufacturing operation which is especially suitable for producing larger size sutures, e.g., those of sizes 3/0 and larger. Extruder unit 10 is of a known or conventional type and is equipped with controls for regulating the temperature of barrel 11 in various zones thereof, e.g., progressively higher temperatures in three consecutive zones A, B and C along the length of the barrel. Pellets or powder of polyamide resin are introduced to the extruder through hopper 12. Any of the polyamides which are useful for the formation of fibers can be used herein. Representative of such polyamides are polycaprolactam (nylon 6) and polyhexamethylene adipamide (nylon 6,6). Optionally, the polyamide sutured may be dyed.

Motor-driven metering pump 13 delivers extruded resin at a constant rate to spin pack 14 and thereafter through spinneret 15 possessing one or more orifices of desired diameter to provide a molten monofilament 16 which then enters quench bath 17, e.g., containing water, where the monofilament solidifies. The distance monofilament 16 travels after emerging from spinneret 15 to the point where it enters quench bath 17, i.e., the air gap, can vary and can advantageously be from about 0.5 to about 100 and preferably from about 1 to about 20 cm. If desired, a chimney (not shown), or shield, can be provided to reduce the length of air gap, e.g., to from 1 to 10 cm, thereby isolating monofilament 16 from contact by air currents which might otherwise affect the cooling of the monofilament in some unpredictable manner. In general, barrel zone A of the extruder can be maintained at a temperature of from about 215° to 225° C., zone B at from about 220° to 230° C. and zone C at from about 220° to about 235° C. Additional temperature parameters include: metering pump block 13 at from about 220° to about 235° C., spin pack 14 at from about 215° to about 235° C., spinneret 15 at from about 215° to about 235° C. and quench bath at from about 35° to about 45° C.

Entering quench bath 17, monofilament 16 is passed by driven roller 18 over rollers 19 and 20 and thereafter is wrapped around a first godet 21 provided with nip roll 22 to prevent slippage which might otherwise result from the subsequent stretching operation. Monofilament 16 passing from godet 21 is stretched, e.g., with stretch ratios on the order of from about 3:1 to about 5:1 and preferably from about 3.5:1 to about 4.5:1, to effect its orientation and thereby increase its tensile strength. In the stretching operation shown in FIG. 1A, generally suitable for larger size sutures, e.g., sizes 2/0 to 3/0, monofilament 16 is drawn through hot water draw bath 23 by means of second godet 24 which rotates at a higher speed than first godet 21 to provide the desired stretch ratio. The temperature of hot water draw bath 23 is advantageously from about 60° to about 98° C. and preferably is from about 80° to about 95° C.

In the alternative stretching operation shown in FIG. 1B, generally preferred for smaller sutures sizes, e.g., sizes 4/0 to 8/0, monofilament 16 is drawn by second godet 24' through hot air oven chamber 23' at a temperature of from about 100° to about 185° C. and preferably from about 150° to about 170° C. to provide the desired amount of stretch. Following the stretching operation shown in FIGS. 1A or 1B, monofilament 16 is subjected to an on-line annealing (relaxation) operation as a result of which the monofilament shrinks. In the processes of FIGS. 1A and 1B, annealing (relaxation) is accomplished by driving monofilament 16 by third godet 26 through second hot air oven chamber 25 at a temperature of from about 120° to about 180° C. and preferably from about 140° to about 160° C. At these temperatures, monofilament 16 will generally recover to within about 85 to about 97 percent, and preferably to within about 95 percent, of its pre-annealed length to provide the finished suture. The third godet relates at a slower speed than the second godet thus relieving tension on the filament.

If desired, the suture can be dyed. If transportation in bulk is required after dyeing, it is preferable to collect the dyed monofilaments in skeins, not on spools, as the latter can cause damage to the suture (flattening). Logwood extract is a known dye for polyamide sutures and can be used herein. However, other dyes known to be suitable for incorporation in sutures can also be used herein, e.g., D&C Green No. 5 and D&C Blue No. 2 as described in the Handbook of U.S. Colorants for Food, Drugs and Cosmetics, by Daniel M. Marrion, 1979.

It is believed that the superior physical and chemical properties of the polyamide sutures of the present invention are due at least in part to the increased carbon content in the structural units of the higher order polyamide resins used in their manufacture. This results in a decrease in the number of amide linkages in the resin. The hydrophilic amide linkage is not only susceptible to cleavage in an aqueous environment, it also favors hydrogen bonding and consequently an affinity for attracting water to the polymer.

In order that those skilled in the art may be better able to practice the present invention, the following examples are given as an illustration of the preparation and superior characteristics of the polyamide sutures of the present invention. It should be noted that the invention is not limited to the specific details embodied in the examples and further that all parts are be weight.

EXAMPLES 1-3

Table I below sets forth typical conditions for extruding, stretching and annealing (relaxing) various sizes of polyamide monofilament suture in accordance with this invention. All of the monofilament sutures were fabricated from AESNO (a commercially available nylon 12 from ATOCHEM North America, Inc.) having an inherent viscosity of about 1.6 dl/g and a moisture content of less than 0.08 weight percent, and a melt flow index of 3.4 g/10 min. as indicated by the manufacturer.

                  TABLE I                                                          ______________________________________                                         CONDITIONS OF MANUFACTURING VARIOUS SIZES                                      OF HIGHER ORDER POLYAMIDE                                                      MONOFILAMENT SUTURE                                                            Example           1        2        3                                          Suture Size       0        3/0      6/0                                        ______________________________________                                         Process Conditions                                                                               Extrusion Operation                                          extruder screw, rpm                                                                              24       10.8     3.4                                        pump rpm          17.4     6.8      9.85                                       driven roller, rpm                                                                               7        7        8                                          barrel temp., °C., zone A                                                                 200      200      200                                        barrel temp., °C., zone B                                                                 210      210      210                                        barrel temp., °C., zone C                                                                 220      215      215                                        clamp temp., °C.                                                                          215      215      215                                        adapter temp., °C.                                                                        215      215      215                                        pump temp., °C.                                                                           220      218      222                                        block temp., °C.                                                                          220      218      218                                        barrel melt temp., °C.                                                                    218      215      214                                        pump melt temp., °C.                                                                      228      221      218                                        spinneret melt temp., °C.                                                                 230      225      226                                        barrel pressure, psi                                                                             1800     2150     2350                                       pump pressure, psi                                                                               1100     1484     2650                                       spinneret pressure, psi                                                                          4500     3228     2650                                       pump size, cc per revolution                                                                     1.168    1.168    0.16                                       diameter of spinneret                                                                            1.25     1.25     0.5                                        orifices, mm                                                                   no. of spinneret orifices                                                                        4        4        4                                          air gap, cm       3        2        3                                          quench bath temp., °C.                                                                    30       36       30                                         depth of driven roller                                                                           38       37       38                                         filtration, microns                                                                              12       12       12                                                         Stretching (Orienting)                                                         Operation                                                      draw bath temp, °C.                                                                       97       97       --                                         first oven chamber temp, °C.                                                              98       82       135                                        first godet, mpm  10.3     10.3     11.6                                       second godet, mpm 40.7     40.8     45.4                                       draw ratio        4.1      4.1      4.1                                                        Annealing (Relaxing)                                                           Operation                                                      second oven chamber temp, °C.                                                             98       98       98                                         third godet, mpm  39.0     38.9     43.4                                       ______________________________________                                    

COMPARATIVE EXAMPLE 1

Table II below sets forth typical conditions for extruding, stretching and annealing (relaxing) a size 3/0 polyamide 6 monofilament suture. In general, useful polyamides will possess a number average molecular weight of at least about 15,000 and a melt flow index in g/10 min of from about 3 to about 8 and preferred from about 4 to about 6. The suture was manufactured from Capron 8207F (Allied Signal Corp.), a polycaprolactone having a relative viscosity of 73.9 and a moisture content of 0.062 weight percent as indicated by the manufacturer.

                  TABLE II                                                         ______________________________________                                         CONDITIONS OF MANUFACTURING A                                                  POLYAMIDE 6 MONOFILAMENT SUTURE                                                Comparative Example 1                                                          Suture Size         3/0                                                        ______________________________________                                         Process Conditions  Extrusion Operation                                        extruder screw, rpm 22.0                                                       pump rpm            7.65                                                       driven roller, rpm  10                                                         barrel temp., °C., zone A                                                                   220                                                        barrel temp., °C., zone B                                                                   225                                                        barrel temp., °C., zone C                                                                   230                                                        clamp temp., °C.                                                                            225                                                        adapter temp., °C.                                                                          225                                                        pump temp., °C.                                                                             225                                                        block temp., °C.                                                                            225                                                        spinneret temp., °C.                                                                        230                                                        barrel melt temp., °C.                                                                      234                                                        pump melt temp., °C.                                                                        230                                                        spinneret melt temp., °C.                                                                   227                                                        barrel pressure, psi                                                                               2650                                                       pump pressure, psi  2890                                                       spinneret pressure, psi                                                                            2730                                                       pump size, cc per revolution                                                                       1.168                                                      diameter of spinneret                                                                              1.25                                                       orifices, mm                                                                   no. of spinneret orifices                                                                          4                                                          air gap, cm         2                                                          quench bath temp., °C.                                                                      45                                                         depth of driven roller                                                                             25                                                         filtration, microns 12                                                                           Stretching (Orienting)                                                         Operation                                                    draw bath temp, °C.                                                                         80                                                         first oven chamber temp, °C.                                                                --                                                         first godet, mpm    17.6                                                       second godet, mpm   70.1                                                       draw ratio          4.0                                                                          Annealing (Relaxing)                                                           Operation                                                    second oven chamber temp, °C.                                                               150                                                        third godet, mpm    66.4                                                       ______________________________________                                    

COMPARATIVE EXAMPLE 2

A size 3/0 nylon 6 suture was prepared in the matter of Comparative Example 1 except that the suture was dyed with black logwood extract.

The physical properties of the higher order polyamide monofilament sutures of this invention and those of the comparative examples were measured at 73° F. and 50 relative humidity. Measurements of percent elongation, tensile strength and energy were carried out employing an Instron Corporation (Canton, Mass.) Tensile Tester, model no. 4301, equipped with yarn grips and operated with a gauge length of 127 mm and a crosshead speed of 127 mm/min.

The physical properties of the sutures and the procedures employed for their measurement are set forth in Table III as follows:

                  TABLE III                                                        ______________________________________                                         PROCEDURES FOR MEASURING PHYSICAL PROP-                                        ERTIES OF POLYAMIDE MONOFILAMENT SUTURES                                       Physical Property                                                                            Test Procedure                                                   ______________________________________                                         knot pull, tensile                                                                           U.S.P. XXI, tensile strength,                                    strength, kg  sutures (881)                                                    straight pull, kg                                                                            ASTM D-2256, Instron Corporation                                 elongation at break, %                                                                       ASTM D-2256                                                      tensile strength, kg/mm.sup.2                                                                ASTM D-2256, Instron Corporation                                               Series IX Automated Materials                                                  Testing System 1.03A                                             0-5% and 0-10% strain                                                                        ASTM D-2256, Instron Corporation                                 energies, kg-mm                                                                              Series IX Automated Materials                                                  Testing System 1.03A                                             knot security A 2 cm loop is tied with a surgeon's                                           square knot (1 = 1 = 1 = 1) securing                                           the throws at 20% of the USP XXII                                              knot strength for 2/0 nonabsorbable                                            sutures (n = 10 loops per group). The                                          loop is placed next to a cloth-wrapped                                         mandrel rotating at .5 rpm. The fixtures                                       are secured to allow contact of the cloth                                      material against the fourth throw or,                                          top throw, of each knot. The cloth                                             wrapping is moistened with 37° C.                                       water prior to the test and is period-                                         ically remoistened during the test. Each - pass of the                         cloth across the knot (for a                                                   total of 100 passes), the knot is inspected                                    for top throw security. For a knot to be                                       considered secure, the 3 mm ears must                                          not come undone and there must be no                                           relaxation of the knot or loss of the                                          fourth throw.                                                    melt flow     ASTM D-1238                                                      ______________________________________                                    

Table IV below sets forth the physical properties of the size 3/0 polyamide 12 suture of the present invention as compared to those properties of the polyamide 6 suture employing the physical testing procedure set forth in Table II.

                  TABLE IV                                                         ______________________________________                                                       Comp.    Comp.                                                   Physical Property                                                                            Ex. 1    Ex. 2     Ex. 1 Ex. 2                                   ______________________________________                                         Wet strength retention                                                                       80%      81%       105%   99%                                    for knot-pull                                                                  Wet strength retention                                                                       94%      83%       100%  100%                                    for straight-pull                                                              Diameter change                                                                              +5%       0%       +1%   -1%                                     Modulus change                                                                               -49%     -32%      -5%   -6%                                     diameter (mm)  0.230    0.236     0.242                                                                                0.244                                  Wet diameter (mm)                                                                             0.241    0.236     0.245                                                                                0.242                                  knot-pull (kg)                                                                               1.78     1.63      1.48  1.63                                    Wet knot-pull (kg)                                                                           1.42     1.32      1.55  1.61                                    Straight-pull (kg)                                                                           2.09     2.01      2.07  1.83                                    wet straight-pull (kg)                                                                       1.97     1.68      2.09  1.85                                    Energy 0-5% (kg-mm)                                                                          1.04     1.30      2.50  2.18                                    Wet Energy 0-5%                                                                              0.24     0.42      2.69  1.70                                    (kg-mm)                                                                        Energy 0-10% (kg-mm)                                                                         6.56     3.70      10.93 8.53                                    Wet Energy 0-10%                                                                             3.55     2.71      11.00 7.51                                    (kg-mm)                                                                        ______________________________________                                    

As demonstrated in Table IV, the strength retention for both straight pull and knot-pull of the nylon 12 suture when exposed to an aqueous medium containing large quantities of water is much greater than that of a corresponding nylon 6.

The yarn of Example 2 and Comparative Example 2 were placed under 1.8 g/den constant tension in a water bath at ambient temperature. At the time intervals listed below, the percent elongation, or "creep", was measured. Table V further illustrates the physical stability of the nylon 12 suture.

                  TABLE V                                                          ______________________________________                                                    Nylon 6           Nylon 12                                          Creep, %   Comparative Example 2                                                                            Example 2                                         ______________________________________                                         5 min      3.3%              1.1%                                              10 min     4.4%              1.1%                                              30 min     6.1%              1.7%                                              45 min     7.2%              1.7%                                              18 hours   13.2%             2.9%                                              ______________________________________                                    

Table V further illustrates the physical stability of the nylon 12 suture.

Obviously, other modifications and variations of the present invention are possible in light of the above teachings. It is therefore to be understood that changes may be made in particular embodiments of the invention described which are within the full intended scope of the invention as defined by the claims. 

What is claimed is:
 1. A polyamide monofilament suture manufactured from a fiber-forming polyamide homopolymer or copolymer possessing a substantial number of units selected from the group consisting of units of the structure in which n is at ##STR5## at least about 7 and units of the structure ##STR6## in which R¹ is an aliphatic group of from about 4 to about 20 carbon atoms, a cycloaliphatic group of from about 6 to about 20 carbon atoms or an aromatic group of from about 6 to about 20 carbon atoms and R² is an aliphatic, cycloaliphatic or aromatic group of from about 6 to about 20 carbon atoms, provided, R¹ contains at least 6 carbon atoms when R² is an aliphatic group of 6 carbon atoms or R² contains at least 8 carbon atoms when R¹ contains 4 carbon atoms, provided, that where the polyamide is a copolymer, any units other than the aforesaid units which may be present contain a carbonyl, the suture being manufactured from the polyamide by an extrusion process which comprises the steps of extruding the polyamide resin at an extrusion temperature of from about 180° to about 290° C. to provide a monofilament, stretching the solidified monofilament at a temperature of from about 40° to about 98° C. in liquid medium or at from about 50° to about 185° C. in gaseous medium at a stretch ratio of from about 3:1 to about 5:1 to provide a stretched monofilament and annealing the stretched monofilament at a temperature of from about 100° to about 240° C. to provide the finished suture, the annealing resulting in shrinkage of the stretched monofilament for a recovery to within about 80% to about 97% of the length of the monofilament prior to annealing, said monofilament having a decreased 0-5% energy compared to a cold-drawn monofilament of the same size and composition.
 2. The suture of claim 1 wherein the polyamide contains at least about 30 mole percent of the units.
 3. The suture of claim 1 wherein the polyamide contains at least about 50 mole percent of the units.
 4. The suture of claim 1 wherein the polyamide contains at least about 70 mole percent of the units.
 5. The suture of claim 1 wherein R¹ is about C₄ aliphatic and R² is about C₁₀ aliphatic.
 6. The suture of claim 1 wherein R¹ is about C₄ aliphatic and R² is about C₁₂ aliphatic.
 7. The suture of claim 1 wherein R¹ is about C₈ aliphatic and R² is about C₈ aliphatic.
 8. The suture of claim 7 wherein R¹ is about C₆ aliphatic and R² is about C₄₋₈ aliphatic.
 9. The suture of claim 1 wherein R¹ is about C₆ aliphatic and R² is about C₁₂ aliphatic.
 10. The suture of claim 1 containing up to about 1 percent by weight of material selected from the group consisting of dyes and pigments.
 11. The suture of claim 1 wherein the units containing a carbonyl are derived from at least one member selected from the group consisting of lactone, alpha-hydroxy carboxylic acid, oligomer of alpha-hydroxy carboxylic acid, aminocarboxylic acid and lactam.
 12. The suture of claim 1 exhibiting not more than about 6 percent creep in an aqueous medium under 1.8 g/den tension.
 13. The suture of claim 1 exhibiting at least about 85 percent wet strength retention for knot pull.
 14. The suture of claim 1 exhibiting at least about 95 percent wet strength retention for straight pull.
 15. A polyamide monofilament suture manufactured from nylon 12, the suture being manufactured by an extrusion process which comprises the steps of extruding the nylon 12 resin at an extrusion temperature of from about 180° to about 290° C. to provide a monofilament, stretching the solidified monofilament at a temperature of from about 40° to about 98° C. in liquid medium or at from about 50° to about 185° C. in gaseous medium at a stretch ratio of from about 3:1 to about 5:1 to provide a stretched monofilament and annealing the stretched monofilament at a temperature of from about 100° to about 240° C. to provide the finished suture, the annealing resulting in shrinkage of the stretched monofilament for a recovery to within about 80% to about 97% of the length of the monofilament prior to annealing, said monofilament having a decreased 0-5% energy compared to a cold-drawn nylon 12 monofilament of the same size.
 16. The suture of claim 15 exhibiting not more than about 6 percent creep in an aqueous medium under 1.8 g/den tension.
 17. The suture of claim 15 exhibiting at least about 85 percent wet strength retention for knot pull.
 18. The suture of claim 15 exhibiting at least about 95 percent wet strength retention for straight pull. 